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Two-step milling process for preparing pigmentary copper phthalocyanine

Assignee: Artience Co Ltd
•
Filing: 1980-03-24
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Granted: 1981-03-24
•
Expires: 2000-03-24
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Abstract

Abstract Converting crude copper phthalocyanine (CPC) to pigmentary copper phthalocyanine (CPC) by two-stage milling with 5-400% by weight of alum and 0.6-3.7 cc of organic liquid per 100 grams of CPC in the first stage and 1.2-9.8 cc of organic liquid per 100 grams of CPC in the second stage with the total organic liquid being 4-13 cc per 100 grams CPC.

Inventors

  • 👤 Howard Matrick

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 07:57
CPC Classifications
C; C09; C09B; C09B67/00; C09B67/0001; C09B67/0014; C09B67/0016; C09B67/0022; C09B67/0023

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 142 words
A two-stage milling process for preparing pigmentary copper phthalocyanine comprising milling crude copper phthalocyanine with a 5-400% by weight of Al 2 (SO 4 ) 3 .15-18 H 2 O based on the crude and 0.6-3.7 cc per 100 grams of copper phthalocyanine of an organic liquid in the first stage, milling said crude further with an additional 1.2-9.8 cc per 100 grams of copper phthalocyanine of an organic liquid in a second stage, the total amount of organic liquid charged in both stages is in the range of 4-13 cc inclusive per 100 grams of copper phthalocyanine, treating the milled copper phthalocyanine with an emulsion of a water-insoluble organic liquid in water with or without a surface-active agent at a temperature of 24°-97° C. for 15 minutes to 10 hours, removing the organic liquid and recovering copper phthalocyanine in pigmentary form.
Claim 2
Dependent Claim 142 words
A two-stage milling process for preparing pigmentary copper phthalocyanine comprising milling crude copper phthalocyanine with a 5-400% by weight of Al 2 (SO 4 ) 3 .15-18 H 2 O based on the crude and 0.6-3.7 cc per 100 grams of copper phthalocyanine of an organic liquid in the first stage, milling said crude further with an additional 1.2-9.8 cc per 100 grams of copper phthalocyanine of an organic liquid in a second stage, the total amount of organic liquid charged in both stages is in the range of 4-13 cc inclusive per 100 grams of copper phthalocyanine, treating the milled copper phthalocyanine with an emulsion of a water-insoluble organic liquid in water with or without a surface-active agent at a temperature of 24°-97° C. for 15 minutes to 10 hours, removing the organic liquid and recovering copper phthalocyanine in pigmentary form.
Claim 3
Dependent Claim 29 words
The process of claim 1 wherein the amount of organic liquid in the first milling stage is 1-3 cc and the amount in the second stage is 2-8 cc.
Claim 4
Dependent Claim 15 words
The process of claim 2 wherein the organic liquid in the milling stages is tetrachloroethylene.
Claim 5
Dependent Claim 23 words
The process of claim 1 wherein the amount of Al 2 (SO 4 ) 3 .15-18 H 2 O is 25-200% by weight.
Claim 6
Dependent Claim 29 words
The process of claim 4 wherein the amount of organic liquid in the first milling stage is 1-3 cc and the amount in the second stage is 2-8 cc.
Claim 7
Dependent Claim 23 words
The process of claim 1 wherein the amount of Al 2 (SO 4 ) 3 .15-18 H 2 O is 50-100% by weight.
Claim 8
Dependent Claim 29 words
The process of claim 6 wherein the amount of organic liquid in the first milling stage is 1-3 cc and the amount in the second stage is 2-8 cc.
Claim 9
Dependent Claim 11 words
The process of claim 1 wherein the organic liquid is tetrachloroethylene.
Claim 10
Dependent Claim 19 words
The process of claim 8 wherein the Al 2 (SO 4 ) 3 .15-18 H 2 O is 25-200%.
Claim 11
Dependent Claim 21 words
The process of claim 8 wherein the Al 2 (SO 4 ) 3 .15-18 H 2 O is 50-100% by weight.
Claim 12
Dependent Claim 20 words
The process of claim 1 wherein the milled copper phthalocyanine is treated in the emulsion formed without a surface-active agent.
Claim 13
Dependent Claim 29 words
The process of claim 11 wherein the amount of organic liquid in the first milling stage is 1-3 cc and the amount in the second stage is 2-8 cc.
Claim 14
Dependent Claim 23 words
The process of claim 11 wherein the amount of Al 2 (SO 4 ) 3 .15-18 H 2 O is 25-200% by weight.
Claim 15
Dependent Claim 23 words
The process of claim 11 wherein the amount of Al 2 (SO 4 ) 3 .15-18 H 2 O is 50-100% by weight.
Claim 16
Dependent Claim 11 words
The process of claim 11 wherein the organic liquid is tetrachloroethylene.

References Cited (Backward Citations)

US2556728A Cited
US2556730A Cited
US3017414A Cited
US3030370A Cited
US3598625A Cited
US4088506A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-03-23 1984-09-22 1985-03-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-03-23 1988-09-22 1989-03-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-03-23 1992-09-22 1993-03-24 $7700.00 Window Closed / Lapsed

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